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JPH082997B2 - Rubber composition containing leather powder and molded article - Google Patents
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JPH082997B2 - Rubber composition containing leather powder and molded article - Google Patents

Rubber composition containing leather powder and molded article

Info

Publication number
JPH082997B2
JPH082997B2 JP2276733A JP27673390A JPH082997B2 JP H082997 B2 JPH082997 B2 JP H082997B2 JP 2276733 A JP2276733 A JP 2276733A JP 27673390 A JP27673390 A JP 27673390A JP H082997 B2 JPH082997 B2 JP H082997B2
Authority
JP
Japan
Prior art keywords
powder
leather powder
leather
rubber
water
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP2276733A
Other languages
Japanese (ja)
Other versions
JPH04149254A (en
Inventor
治規 甲斐
隆夫 井ノ口
透 西
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Idemitsu Petrochemical Co Ltd
Original Assignee
Idemitsu Petrochemical Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Idemitsu Petrochemical Co Ltd filed Critical Idemitsu Petrochemical Co Ltd
Priority to JP2276733A priority Critical patent/JPH082997B2/en
Priority to US07/776,076 priority patent/US5272190A/en
Priority to TW080108055A priority patent/TW218886B/zh
Priority to AU85821/91A priority patent/AU639149B2/en
Priority to KR1019910018027A priority patent/KR0128515B1/en
Priority to DE69119349T priority patent/DE69119349T2/en
Priority to EP91117582A priority patent/EP0481430B1/en
Publication of JPH04149254A publication Critical patent/JPH04149254A/en
Publication of JPH082997B2 publication Critical patent/JPH082997B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/18Manufacture of films or sheets
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L7/00Compositions of natural rubber
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L21/00Compositions of unspecified rubbers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/16Ethylene-propylene or ethylene-propylene-diene copolymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L83/00Compositions of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon only; Compositions of derivatives of such polymers
    • C08L83/04Polysiloxanes
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L89/00Compositions of proteins; Compositions of derivatives thereof
    • C08L89/04Products derived from waste materials, e.g. horn, hoof or hair
    • C08L89/06Products derived from waste materials, e.g. horn, hoof or hair derived from leather or skin, e.g. gelatin

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Dermatology (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Treatment And Processing Of Natural Fur Or Leather (AREA)
  • Synthetic Leather, Interior Materials Or Flexible Sheet Materials (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Injection Moulding Of Plastics Or The Like (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は皮革粉含有ゴム組成物及び成形品に関し、テ
ニスラケット、バドミントンラケット、ゴルフクラブ、
野球用バット等におけるグリップ等のスポーツ用品、ゴ
ム製手袋、合羽、帽子等の衣料用品、ハンドル巻皮用バ
ンド、二輪車ハンドル用グリップ、窓枠ゴム、ワイパー
ゴム、防振ゴム、ブレーキゴム、シフトレバー用グリッ
プ、車室内装品、タイヤ等の車両用部品、すべり止め部
材、吸音材等の建材、ゴム靴、靴底等の靴製品の他、家
電製品、文房具、家具、楽器等に利用できる。
TECHNICAL FIELD The present invention relates to a leather powder-containing rubber composition and a molded article, and relates to a tennis racket, a badminton racket, a golf club,
Sports goods such as grips for baseball bats, clothing items such as rubber gloves, feathers, hats, handle leather bands, motorcycle handle grips, window frame rubber, wiper rubber, anti-vibration rubber, brake rubber, shift lever It can be used for vehicle grips, vehicle interior parts, vehicle parts such as tires, non-slip members, building materials such as sound absorbing materials, rubber shoes, shoe products such as shoe soles, as well as home appliances, stationery, furniture, musical instruments and the like.

〔背景技術〕[Background technology]

近年、天然皮革のもつ吸放湿性と、しっとりとした高
級感のある手触りに、人工皮革のもつ強度を合せもった
素材として、合成樹脂と天然皮革粉末とを混合一体化し
た素材(組成物)が開発されている。
In recent years, a material (composition) in which synthetic resin and natural leather powder are mixed and integrated as a material that combines the moisture absorption and desorption properties of natural leather with the moist and high-class feel to the strength of artificial leather. Is being developed.

また、天然皮革粉末を合成ゴムや天然ゴム等と混合一
体化する技術どして、特開昭53−121902号や特開昭62−
252459号公報が知られている。これらは、ゴム単体では
見られない吸、放湿性を付与する技術である。
Further, as a technique for mixing and integrating natural leather powder with synthetic rubber, natural rubber, etc., Japanese Patent Laid-Open Nos. 53-121902 and 62-62
No. 252459 is known. These are technologies that impart absorption and moisture release properties that cannot be seen with rubber alone.

〔発明が解決しようとする課題〕 しかしながら、これらの技術で得られる天然皮革粉含
有ゴム組成物及び成形品においては、長期間の使用や保
存、特に多湿雰囲気中での長期間の放置により、その表
面に白粉が生じ、製品の性能や品質(外観)を低下させ
るという欠点があった。特に、天然皮革粉として粒径の
小さい、例えば、250μm以下の粒径のものを用いる
と、白粉の発生が著しかった。
[Problems to be Solved by the Invention] However, in the natural leather powder-containing rubber composition and molded article obtained by these techniques, long-term use and storage, especially by leaving for a long time in a humid atmosphere, There is a drawback that white powder is generated on the surface and the product performance and quality (appearance) are deteriorated. In particular, when a natural leather powder having a small particle size, for example, a particle size of 250 μm or less was used, generation of white powder was remarkable.

また、天然皮革粉含有ゴム組成物を用いてスポーツ用
品のグリップを作製する場合、表面形状を良好にするた
め、表面研磨をすると、天然皮革粉の平均粒径が小さ
い、例えば10μm未満であると、皮革粉による吸湿量が
多少劣り、同じ含有量のものに比べすべり防止効果が少
なくなってしまい、全体の特性バランスが悪くなってし
まうという問題点を生ずる。
Further, in the case of producing a grip for sports equipment using a rubber composition containing natural leather powder, if the surface is ground to improve the surface shape, the average particle size of the natural leather powder is small, for example, less than 10 μm. However, the moisture absorption by the leather powder is somewhat inferior, the slip prevention effect is less than that of the same content, and the overall property balance is deteriorated.

本発明の目的は、白粉の発生のない優れた長期性能及
び品質を有する皮革粉含有ゴム組成物及び成形品を提供
するにある。
An object of the present invention is to provide a leather powder-containing rubber composition and a molded article having excellent long-term performance and quality without generation of white powder.

〔課題を解決するための手段および作用〕[Means and Actions for Solving the Problems]

本発明は、皮革粉含有ゴム組成物を用いた成形品の製
品化において、不純物の少ない特定粒径の微細皮革粉を
使用することが白粉の発生を防止できることに着目し、
これにより前記目的を達成しようとするものである。
The present invention, in the commercialization of molded articles using a leather powder-containing rubber composition, paying attention to the fact that it is possible to prevent the generation of white powder by using fine leather powder of a small particle size with less impurities,
This is intended to achieve the above object.

本発明の皮革粉含有ゴム組成物は、皮質分が75wt%以
上、水で抽出可能なNa+イオンとCa2+イオンとの合計量
が0.5wt%以下、及び平均粒径D50が10μm〜250μmで
ある皮革粉10〜400重量部と、ゴム100重量部との分散混
合物から構成される。
The leather powder-containing rubber composition of the present invention has a cortical content of 75 wt% or more, a total amount of water-extractable Na + ions and Ca 2+ ions of 0.5 wt% or less, and an average particle diameter D 50 of 10 μm to. It is composed of a dispersed mixture of 10 to 400 parts by weight of leather powder of 250 μm and 100 parts by weight of rubber.

また、本発明の皮革粉含有ゴム成形品は、前述の皮革
粉含有ゴム組成物を主として用いて形成される。
Further, the leather powder-containing rubber molded article of the present invention is formed mainly using the above-mentioned leather powder-containing rubber composition.

本発明の皮革粉含有ゴム組成物及び成形品は、基本的
には、ゴム中に皮革粉が海島状に分散されたものであ
る。
The leather powder-containing rubber composition and the molded article of the present invention are basically rubber powder in which leather powder is dispersed in a sea-island shape.

このタイプの組成物及び成形品において、皮革粉材料
の及びゴム材料の使用量は、それぞれ、10〜400重量部
及び100重量部である。皮革粉の割合が400重量部を超え
ると、組成物において混練撹拌が困難になり、均一に分
散できなくなって成形品に脆化が現れる。また、10重量
部未満ではその添加効果、すなわち吸、放湿性等が不十
分となる。
In this type of composition and molded article, the amounts of leather powder material and rubber material used are 10 to 400 parts by weight and 100 parts by weight, respectively. If the proportion of leather powder exceeds 400 parts by weight, it becomes difficult to knead and stir the composition, and it becomes impossible to uniformly disperse the composition, so that the molded product becomes brittle. On the other hand, if it is less than 10 parts by weight, the effect of its addition, that is, the absorption and moisture releasing properties will be insufficient.

本発明の組成物及び成形品において、皮革粉の特性値
を限定したのは、次のような理由による。
In the composition and molded article of the present invention, the characteristic value of the leather powder is limited for the following reason.

1)皮質分75wt%以上: 皮質分の含有量が多いということは、不純物の量が少
ないことを意味すると同時に、ゴムグリップ、ゴム手袋
等に混入した製品の表面状態、タッチ感等を向上させる
重要な因子となることを意味する。即ち、皮質分が多い
方が少ない粉末量で効率的に製品の表面状態等を改善で
きる。
1) Cortical content 75 wt% or more: A high content of cortical content means that the amount of impurities is low, and at the same time improves the surface condition and touch feeling of products mixed in rubber grips, rubber gloves, etc. It is meant to be an important factor. That is, the surface state and the like of the product can be efficiently improved with a smaller amount of powder having a larger cortical content.

2)水で抽出可能な遊離イオン(Na+,Ca2+)の合計量0.
5wt%以下: 皮革原料に由来する不純物のうち、水で抽出された遊
離イオン量が多いと、製品化した場合、湿度、熱等の影
響を受け、製品表面にその塩(例えばNaCl,Na2So4、CaS
O4等)がブリードアウトし、製品外観の悪化につなが
る。
2) Total amount of free ions (Na + , Ca 2+ ) that can be extracted with water.
5 wt% or less: Of the impurities derived from leather raw materials, if the amount of free ions extracted with water is large, it will be affected by humidity, heat, etc. when commercialized, and its salts (eg NaCl, Na 2 So 4 , CaS
O 4 etc.) bleed out, leading to a deterioration of the product appearance.

なお、水で抽出可能な遊離イオンとしては、Na+,Ca2+
の陽イオンの他に、Cl-,SO4 2-の陰イオンも存在する
が、ブリードアウトしてくるものは、それらイオンの対
イオンの塩の形態でしか生じないため、量の少ない陽イ
オンであるNa+とCa2+との合計量で規定した。
The free ions that can be extracted with water include Na + and Ca 2+.
In addition to the anions of Cl - and SO 4 2- , there are also anions of Cl - and SO 4 2- , but bleeding-out anions are formed only in the form of the salt of the counterion of those ions. Is defined as the total amount of Na + and Ca 2+ .

3)平均粒径D50=10〜250μm: 平均粒径は、10μm未満では、吸、放湿性が小さく、
特に、成形品を研磨したとき、十分なすべり止め効果を
発揮できない。一方、250μmを越えると、分散不良に
よる欠陥及び表面風合の悪化(ザラザラ感、凹凸感)に
つながる。
3) Average particle size D 50 = 10 to 250 μm: When the average particle size is less than 10 μm, the water absorption and moisture releasing properties are small,
In particular, when the molded product is polished, it cannot exert a sufficient anti-slip effect. On the other hand, when it exceeds 250 μm, it leads to defects due to poor dispersion and deterioration of surface texture (roughness, unevenness).

なお、皮革粉の代わりにゼラチンを用いた場合は、表
面がベトツキ好ましくない。
When gelatin is used instead of leather powder, the surface is not sticky.

また、皮革粉中の油脂分は、成形品の臭いに関係する
が、本発明に係る組成物及び成形品は、ゴムを含んでお
り、コムの臭いがかなり強いため、皮革粉中の脱脂は必
ずしも必要ない。しかし、脱脂をして皮革粉中の油脂分
を少なくすれば、皮革粉中の油脂分が熱等で変質して生
ずる悪臭や、着色及びブリードアウトによる表面風合の
劣化を少なくできるから、好ましくは油脂分2wt%以
下、より好ましくは0.5wt%を以下に脱脂するのがよ
い。
Further, the oil and fat content in the leather powder is related to the odor of the molded article, but the composition and the molded article according to the present invention contain rubber, and because the smell of the comb is considerably strong, the degreasing in the leather powder is Not necessarily required. However, if the oil and fat content in the leather powder is reduced by degreasing, a bad odor caused by the oil and fat content in the leather powder being deteriorated by heat or the like, and the deterioration of the surface texture due to coloring and bleed-out can be reduced, which is preferable. The oil content should be degreased to 2 wt% or less, more preferably 0.5 wt% or less.

上記特性値の測定法は、次の通りである。 The method for measuring the above characteristic values is as follows.

A)皮質分: JIS K6550−1976「皮革試験方法」6.7による。A) Cortical component: According to JIS K6550-1976 "Leather test method" 6.7.

B)水で抽出可能な遊離イオン(Na,Ca2+)の合計量: 乾燥皮革粉10gを純水100ml中で一昼夜撹拌し、皮革粉
中の遊離インを抽出する。抽出液中のNa+,Ca2+を原子吸
光法定量し、皮革粉からの抽出量として求める。
B) Total amount of free ions (Na, Ca 2+ ) extractable with water: 10 g of dried leather powder is stirred in 100 ml of pure water for 24 hours to extract free in from the leather powder. The amount of Na + and Ca 2+ in the extract is determined by atomic absorption spectrometry, and the amount extracted from the leather powder is determined.

C)平均粒径 数十mgの皮革部を100mlのメタノールに分散し、コー
ルターカウンター(コールター・エレクトロニクス社
製)で粒子の分布を測定し、平均粒径を求める。
C) Average particle size A leather part of several tens of mg is dispersed in 100 ml of methanol, and the particle distribution is measured with a Coulter counter (manufactured by Coulter Electronics Co.) to obtain the average particle size.

なお、皮革粉を120℃で2時間乾燥後、JIS K6721に準
じて測定する皮革粉の密度範囲は、通常0.38g/cc以上で
ある。密度が小さ過ぎると、皮革粉が繊維状となった
り、セン毛部分が多く出てゴムと均一に分散し難くなる
ことがあるからである。
The density range of the leather powder measured according to JIS K6721 after the leather powder is dried at 120 ° C. for 2 hours is usually 0.38 g / cc or more. This is because if the density is too low, the leather powder may become fibrous, or a large amount of loose hairs may appear to make it difficult to uniformly disperse the rubber in the rubber.

以上のような本発明に使用される皮革粉は、例えば皮
革粉原料に対し粗粉砕、水洗、脱水、スチームによる膨
潤処理、乾燥、微粉砕を行って得ることができる。この
後、必要に応じて分級の工程を行って、使用目的に応じ
た平均粒径の皮革粉を分離することもできる。また、皮
革粉の脱脂を行うには、粗粉砕と水洗との工程の間に、
乾燥、溶剤による脱脂、残存溶剤の除去等の工程介装す
ればよい。
The leather powder used in the present invention as described above can be obtained, for example, by subjecting the leather powder raw material to coarse pulverization, washing with water, dehydration, swelling treatment with steam, drying and fine pulverization. Then, if necessary, a classification step may be performed to separate the leather powder having an average particle diameter according to the purpose of use. In addition, in order to degrease the leather powder, between the steps of coarse grinding and washing with water,
It suffices to perform steps such as drying, degreasing with a solvent, and removal of residual solvent.

この製造方法をさらに詳しく説明すると、まず後工程
の微粉砕を容易にするため、皮革粉原料をジョークラッ
シャー、カッターミル、ハンマークラッシャー等の粗砕
機で粒径10mm以下程度に粗粉砕する。こうして得られる
粗砕皮革粉は、通常40〜60wt%の水分を含んでいる。
This manufacturing method will be described in more detail. First, in order to facilitate fine pulverization in the subsequent step, the leather powder raw material is coarsely pulverized to a particle size of 10 mm or less by a pulverizer such as a jaw crusher, a cutter mill, a hammer crusher. The roughly crushed leather powder thus obtained usually contains 40 to 60% by weight of water.

なお、皮革粉原料としてはシェービング屑革、床革等
が使用できる。
As the leather powder raw material, shaving waste leather, floor leather, etc. can be used.

次に、主として皮革中の遊離イオン(Na+,Ca2+)を抽
出、除去すると共に、粗粉末に所定の水分を保持させる
ため、水洗工程及び脱水工程からなる一連の水洗操作を
行う。
Next, in order to mainly extract and remove free ions (Na + , Ca 2+ ) in the leather and to retain a predetermined water content in the coarse powder, a series of water washing operations including a water washing step and a dehydration step is performed.

一連の水洗操作は、バッチ式で数回繰り返す方法が効
果的で、例えば溶剤除去後の粗粉末に一定量の水を供給
し、所望時間撹拌及び必要あれば空気によるバブリング
を行った後、脱水する方法を、水の供給量にもよるが、
通常数回、好ましくは3〜4回り返す。脱水は、通常、
操作の簡便性の点から濾過(水切り又は水抜き)により
行なわれるが、遠心脱水等、他の方法で行なってもよ
い。
A series of water washing operations is effective in a method of repeating several times in a batch system, for example, a certain amount of water is supplied to the crude powder after solvent removal, and after stirring for a desired time and bubbling with air if necessary, dehydration is performed. How to do it depends on the amount of water supplied,
It is usually repeated several times, preferably 3 to 4 times. Dehydration is usually
Although filtration (draining or draining) is carried out from the viewpoint of ease of operation, it may be carried out by another method such as centrifugal dehydration.

なお、連続式水洗操作は使用水量が多くなり、有利と
は言えないが、可能である。
It should be noted that the continuous washing operation uses a large amount of water and is not advantageous, but it is possible.

水温は、常温でよく、好ましくは30℃以下である。 The water temperature may be room temperature, preferably 30 ° C or lower.

以上の一連の水洗操作により、遊離のNa+イオンとCa
2+イオンとの合計量(乾燥重量換算)が0.5wt%以下
で、水分が通常65〜70%の含水粗粉末が得られる。この
一連の水洗操作により、最終的に粗粉末は、通常、所定
の水分(65〜70%)を保持することになる。
By the above series of washing with water, free Na + ions and Ca
A water-containing coarse powder having a total amount of 2+ ions (dry weight conversion) of 0.5 wt% or less and a water content of 65 to 70% is usually obtained. By this series of water washing operations, the coarse powder finally retains a predetermined water content (65 to 70%).

従って、この方法は、脱水後の粗粉末の水分の確認だ
けでよく、従来行われているような、溶剤除去後の粗粉
末に所定の水分になる迄、水を補給する調湿工程を事実
上廃止できるという利点がある。
Therefore, this method only requires confirmation of the water content of the coarse powder after dehydration, and the conventional humidity control step of replenishing the coarse powder after solvent removal with water until the desired water content is achieved. The advantage is that it can be abolished.

ここで、粗粉末に所定量の水分を保持又は補給するの
は、次のような理由による。即ち、乾いた状態では、次
工程のスチーム蒸煮後微粉砕を行っても、微粉化が進ま
ない。しかし、水分を含み、従って膨潤した粗粉末をス
チーム蒸煮すると、一部熱変性し、乾燥すると、締まっ
て固くなり、粉砕、微粉化がし易くなるからである。
Here, the reason why the predetermined amount of water is retained or supplied to the coarse powder is as follows. That is, in the dry state, even if finely pulverized after steam steaming in the next step, pulverization does not proceed. However, when steam-cooking a coarse powder containing water and thus swollen, it is partially heat-denatured, and when it is dried, it becomes tight and hard, and is easily crushed and pulverized.

次に、後工程の微粉砕を容易にするため、脱水後の粗
砕皮革粉を撹拌しながら、スチームにより膨潤処理(ス
チーム蒸煮)を行う。
Next, in order to facilitate the fine pulverization in the subsequent step, swelling treatment (steam steaming) is performed with steam while stirring the coarsely crushed leather powder after dehydration.

引続き、後工程の微粉砕を容易にするため、膨潤処理
後の粗砕皮革粉を水分3wt%以下程度になる迄、乾燥す
る。この乾燥工程は、通常、ドライヤーによる予備乾燥
及び真空乾燥機による本乾燥を組み合わせて行われる。
Subsequently, in order to facilitate the fine pulverization in the subsequent step, the coarsely crushed leather powder after the swelling treatment is dried until the water content becomes about 3 wt% or less. This drying step is usually performed by combining preliminary drying with a dryer and main drying with a vacuum dryer.

次に、乾燥後の粗砕皮革粉をビクトリーミル、ボール
ミル、コロイドミル、ジェットミル、ローラミル、ハン
マーミル等の乾式粉砕機で、平均粒径10μm〜250μm
程度になる迄、微粉砕する。
Next, the coarsely crushed leather powder after drying is dried with a dry mill such as a Victory mill, ball mill, colloid mill, jet mill, roller mill, or hammer mill to have an average particle size of 10 μm to 250 μm.
Finely grind until it reaches a certain level.

次に、必要に応じて、得られた広い粒径範囲をもつ微
粉砕皮革粉を重力式分級機;慣性式分級機;サイクロ
ン、ミクロンセパレーター等の遠心式分級機;ふるい分
け機等により、使用目的に応じた種々の平均粒径のもの
に分級してもよい。
Then, if necessary, the obtained finely ground leather powder having a wide particle size range is used by a gravity classifier; an inertial classifier; a centrifugal classifier such as a cyclone, a micron separator; a sieving machine, etc. The particles may be classified into various average particle sizes according to the above.

なお、皮革粉の脱脂を行うには、例えば、粗粉砕と水
洗との工程の間に、次の次工程を加入する。
In order to degrease the leather powder, for example, the following next step is added between the steps of coarse pulverization and washing with water.

すなわち、後工程での脱脂(油脂分の除去)を容易に
するため、含水粗粉末を20〜30wt%程度の水分になる
迄、乾燥する。
That is, in order to facilitate degreasing (removal of oil and fat) in a later step, the water-containing coarse powder is dried until the water content becomes about 20 to 30 wt%.

次に、この乾燥粗粉末を適当な溶剤を用いて油脂分が
好ましくは2wt%以下、より好ましくは0.5wt%以下にな
る迄、脱脂する。ここで、脱脂用溶剤としてn−ヘキサ
ン、ベンジン、メチレンクロライド、アセトン、酢酸エ
チル、トルエン等が使用できる。
Next, the dried crude powder is degreased with a suitable solvent until the fat and oil content is preferably 2 wt% or less, more preferably 0.5 wt% or less. Here, n-hexane, benzine, methylene chloride, acetone, ethyl acetate, toluene or the like can be used as the degreasing solvent.

引続き、粗粉末中の残存溶剤を除去するため、脱脂後
の粗粉末を熱処理する。熱源としては、通常、安全上か
らスチーム(水蒸気)が使用されるため、この工程はス
チームパージとも呼ばれる。他の熱源としては加熱窒
素、加熱空気等も使用できる。
Subsequently, in order to remove the residual solvent in the coarse powder, the coarse powder after degreasing is heat-treated. Since steam (steam) is usually used as a heat source for safety reasons, this process is also called steam purge. As other heat source, heated nitrogen, heated air, etc. can be used.

以上の脱脂をする方法では、一連の水洗操作を脱脂工
程の後で行ったが、この水洗操作は脱脂の前あるいは微
粉化後でも可能である。
In the above degreasing method, a series of water washing operations are performed after the degreasing step, but this water washing operation can be performed before degreasing or after pulverization.

以上のようにして得られる皮革粉と併用されるゴムと
しては、ジエン系(ブタジエン−スチレン、ブタジエン
−アクリロニトリル)、多硫化物系(チオコール)、オ
レフィン系(エチレン−プロピレン、クロルスルホン化
ポリエチレン)、有機ケイ素化合物系、含フッ素化合物
系、ウレタン系、ビニル系等の合成ゴムや、天然ゴムが
ある。
The rubber used in combination with the leather powder obtained as described above includes diene (butadiene-styrene, butadiene-acrylonitrile), polysulfide (thiochol), olefin (ethylene-propylene, chlorosulfonated polyethylene), There are synthetic rubbers such as organosilicon compound-based, fluorine-containing compound-based, urethane-based, vinyl-based and natural rubbers.

これらの各種の合成及び/又は天然ゴムは、単独で用
いるものの他、複数を混合して用いてもよい。
These various synthetic and / or natural rubbers may be used alone or in combination of two or more.

本発明の組成物には、改質、品質の安定化等の目的や
使用目的、使用環境に応じて、この分野で通常使用され
る添加剤、例えば、加硫剤、加硫促進剤、加硫促進助
剤、加工助剤の他、染料、顔料等の着色剤、紫外線吸収
剤、老化防止剤等を任意に必要量添加することができ
る。
The composition of the present invention contains additives commonly used in this field, such as a vulcanizing agent, a vulcanization accelerator, and a vulcanization accelerator, depending on the purpose of modification, stabilization of quality, the purpose of use, the use environment. In addition to a sulfur-accelerating aid, a processing aid, a coloring agent such as a dye or a pigment, an ultraviolet absorber, an antiaging agent and the like can be optionally added in necessary amounts.

ここで、加硫剤としては、粉末イオウ、不溶性イオ
ウ、表面処理イオウ等のイオウ;酸化マグネシウム、亜
鉛等(CR,CSM,T用)等の金属酸化物;キノイド加硫剤;
過酸物加硫剤;アミン加硫剤;樹脂加硫剤;有機イオウ
加硫剤等がある。
Here, as the vulcanizing agent, sulfur such as powdered sulfur, insoluble sulfur, surface-treated sulfur and the like; metal oxide such as magnesium oxide, zinc and the like (for CR, CSM, T); quinoid vulcanizing agent;
Peracid vulcanizing agents; amine vulcanizing agents; resin vulcanizing agents; organic sulfur vulcanizing agents and the like.

加硫促進剤としては、ジチオカルバミン酸鉛塩、複素
環式メルカプタン等がある。
Examples of the vulcanization accelerator include lead dithiocarbamic acid salt and heterocyclic mercaptan.

加硫促進助剤としては、亜鉛華、ステアリン酸等があ
る。
Examples of the vulcanization accelerator include zinc white and stearic acid.

加工助剤としては、ステアリン酸、ポリエチレングリ
コール、パラフィンワックス等がある。
Processing aids include stearic acid, polyethylene glycol, paraffin wax and the like.

紫外線吸収剤としては、フェニルサリチレートのよう
なサリチル酸エステル系;2−ヒドロキシフェニルベンゾ
リアゾールのようなベンゾトリアゾール系;2−ヒドロキ
シベンゾフェノン、2−ヒドロキシ−4−メトキシベン
ゾフェオン、2−ヒドロキシ−4−オクトキシベンゾフ
ェノン、2,2′−ジヒドロキシ−4−メトキシベンゾフ
ェノン等のヒドロキシベンゾフェノン系等がある。
As the ultraviolet absorber, salicylic acid ester such as phenyl salicylate; benzotriazole such as 2-hydroxyphenyl benzotriazole; 2-hydroxybenzophenone, 2-hydroxy-4-methoxybenzopheon, 2-hydroxy There are hydroxybenzophenone compounds such as -4-octoxybenzophenone and 2,2'-dihydroxy-4-methoxybenzophenone.

以上のような材料を用いて、本発明の皮革粉含有ゴム
組成物及び成形品を製造する方法としては、一般の混合
方法を用いることができるが、次のようにしてもよい。
As a method for producing the leather powder-containing rubber composition and the molded article of the present invention using the above-mentioned materials, a general mixing method can be used, but the following method may also be used.

予め30〜60℃に温度調節されたバンバリーミキサー等
で、細く裁断されたゴムを溶融しておき、皮革粉末を追
加混合するか、あるいは、両原料を同時にミキサーへ投
入し、混合する。
The finely cut rubber is melted in advance with a Banbury mixer or the like whose temperature is adjusted to 30 to 60 ° C., and the leather powder is additionally mixed, or both raw materials are simultaneously added to the mixer and mixed.

混合したものは、更に、二本ロールで30〜40℃にてシ
ート状にし、シート状成形品を得、あるいは、所定の型
内に注入又は付着させて所定形状の成形品を得る。
The mixed product is further made into a sheet by a two-roll at 30 to 40 ° C. to obtain a sheet-shaped molded product, or by pouring or adhering it into a predetermined mold to obtain a molded product having a predetermined shape.

また、液状のゴムを用いるときは、撹拌翼等により、
液状ゴムと皮革粉末とを混合する。
Also, when using liquid rubber, use a stirring blade, etc.
Mix liquid rubber and leather powder.

ここで、採用できる代表的な成形法には、射出成形、
中空(吹込)成形、圧縮成形、回転成形、パウダースラ
ッシュ成形等がある。
Here, typical molding methods that can be adopted are injection molding,
Hollow (blown) molding, compression molding, rotational molding, powder slush molding, etc. are available.

また、皮革粉とゴムとの混練には、バンバリーミキサ
ーの他に、押出機、練ロール等を用いることができ、ゴ
ムの素材としては、裁断したブロック状の他に、ペレッ
ト状、パウダー状等でもよい。
Further, for kneading the leather powder and the rubber, an extruder, a kneading roll or the like can be used in addition to the Banbury mixer, and the material of the rubber is not only a cut block but also a pellet, a powder, etc. But it's okay.

〔実施例〕〔Example〕

以下、本発明を実施例によってさらに詳しく説明す
る。
Hereinafter, the present invention will be described in more detail with reference to Examples.

まず、皮革粉の製造方法について説明する。 First, a method for manufacturing leather powder will be described.

クロムなめしした牛皮屑革(シェービング革)の塊12
00kgを解砕機(ホソカワミクロン社製)で、元のシェー
ビング屑革の形状(max:1cm幅×12cm長)にほぐした
後、粗砕機(オダテ社製ハンマーミル:能力600kg/Hr)
に順次送り込み、粒径約10mm以下の粗砕皮革粉とする。
この粗粉末の水分は40〜60wt%であった。
A lump of chrome-tanned cowhide leather (shaving leather) 12
After crushing 00kg into the shape of the original shaving waste leather (max: 1cm width x 12cm length) with a crusher (made by Hosokawa Micron), a coarse crusher (hammer mill made by Odate: capacity 600kg / hr)
Sequentially, to make coarsely crushed leather powder with a particle size of about 10 mm or less.
The water content of this coarse powder was 40 to 60 wt%.

次に、より良好な皮革粉を得るため樹脂をするが、こ
の脱脂は次のようにして行った。
Next, a resin is applied to obtain a better leather powder, and this degreasing was performed as follows.

すなわち、湿潤粗砕皮革粉350kgを真空乾燥機に入
れ、水分が20〜30wt%になる迄、乾燥する。引続き、こ
の乾燥粗砕皮革粉270kgを脱脂機に投入し、n−ヘキサ
ンを100/minでフィードしながら、1時間15分撹拌、
抽出を行って脱脂した後、濾過する。得られた脱脂粗粉
末中の残存油脂分は、0.5wt%以下であった。
That is, 350 kg of wet coarse crushed leather powder is put in a vacuum dryer and dried until the water content becomes 20 to 30 wt%. Subsequently, 270 kg of this dried and roughly crushed leather powder was put into a degreasing machine, and while feeding n-hexane at 100 / min, stirring for 1 hour and 15 minutes,
Extract and degrease, then filter. The residual oil and fat content in the obtained defatted coarse powder was 0.5 wt% or less.

次に、この脱脂粗砕皮革粉柱の残存溶剤を130℃,2kg/
cm2Gの水蒸気で溶剤(ヘキサン)臭がなくなるまでパー
ジし、脱脂関連工程を完了する。
Next, the residual solvent of this defatted coarsely crushed leather powder column was heated at 130 ° C, 2 kg /
Purge with cm 2 G of steam until the odor of the solvent (hexane) disappears, and complete the degreasing-related steps.

同脱脂機に常温の水2m2を補給し、30分撹拌後、濾過
により水切りする。このバッチ水洗操作を計4回行っ
て、屑革中の金属イオン等の遊離イオン及び水溶性成分
を除去する。濾過、水切り後の粗砕皮革粉は65〜70wt%
の水分を含んでいた。
The degreasing machine is replenished with 2 m 2 of room temperature water, stirred for 30 minutes, and then drained by filtration. This batch washing operation is carried out four times in total to remove free ions such as metal ions and water-soluble components in the scrap leather. 65-70wt% of coarsely crushed leather powder after filtration and draining
It contained water.

次に、これを調湿することなく、スチーム蒸煮機に移
し、撹拌しながら130℃,2kg/cm2Gの水蒸気で45分間蒸煮
する。
Next, this is transferred to a steam steamer without humidity control, and steamed at 130 ° C. and 2 kg / cm 2 G of steam for 45 minutes while stirring.

次に、蒸煮後の粗砕皮革粉を、90℃に保持されたドラ
イヤーで30〜40wt%の水分になるまで3時間予備乾燥し
た後、真空乾燥機で45℃、8時間乾燥し、水分1wt%以
下の乾燥粗砕皮革粉190kgを得る。
Next, the steamed coarsely crushed leather powder is pre-dried for 3 hours with a dryer kept at 90 ° C until the water content becomes 30-40wt%, and then dried with a vacuum dryer at 45 ° C for 8 hours to obtain a water content of 1wt. 190 kg of dry coarsely crushed leather powder of not more than% is obtained.

次に、これをファインビクトリーミル(ホソカワミク
ロン社製)で、2時間、1700rpmで微粉砕する。
Next, this is finely pulverized at 1700 rpm for 2 hours with a Fine Victory Mill (manufactured by Hosokawa Micron).

引続き、これをサイクロン式分級機で分級し、平均粒
計D50=約30μmの微細皮革粉35kg及びD50=約60μmの
粗大皮革粉155kgを得る。
Subsequently, this is classified by a cyclone classifier to obtain 35 kg of fine leather powder with an average particle size D 50 = about 30 μm and 155 kg of coarse leather powder with D 50 = about 60 μm.

成形品の製造: 実施例1 天然ゴム(#3)50重量部、合成ゴム・EPDM(エチレ
ン・プロヒレン・ジエン・メチレン・リンケージ;出光
ディーエスエム社Keltan314)50重量部の各々を約3cm角
のブロックに切断し、約40℃に加温されたバンバリーミ
キサーにより溶融後、前述のように処理して得られた50
重量部の天然皮革粉のうち平均粒径60μmのプロテイン
パウダーを添加混合した。
Manufacture of molded product: Example 1 50 parts by weight of natural rubber (# 3) and 50 parts by weight of synthetic rubber / EPDM (ethylene / pro-lene / diene / methylene linkage; Keltan 314 of Idemitsu DSM Co., Ltd.) each of about 3 cm square block. 50 pieces obtained by cutting into pieces, melting with a Banbury mixer heated to about 40 ° C, and treating as described above
Protein powder having an average particle size of 60 μm was added and mixed in parts by weight of natural leather powder.

混練物は、更に約50℃の二本ロールにより、厚さ1cm
位のイート状に形成し、自然冷却した。
The kneaded product is further rolled by a two-roll roll at about 50 ° C to a thickness of 1 cm.
It was formed into a sheet-shaped sheet and naturally cooled.

この混合物シートをさらに2本ロールを用いて加硫し
た後、150℃、5分間プレスし、縦×横×厚さ=150mm×
200mm×2mmの板を成形した。
The mixture sheet was further vulcanized by using two rolls and then pressed at 150 ° C. for 5 minutes to obtain length × width × thickness = 150 mm ×
A 200 mm x 2 mm plate was formed.

混合物シートでは、耐湿テストと切断面の粉落ち(皮
革粉の成形品からの離脱)チェック、更に、成形板では
吸湿量及び動摩擦係数の測定を行ない、成形板の表面を
約20μm研磨したものについても、吸湿量及び動摩擦係
数の測定を行った。
For the mixture sheet, the moisture resistance test and the powder drop on the cut surface (leather powder detachment from the molded product) were checked, and the moisture absorption amount and the dynamic friction coefficient were measured for the molded plate, and the surface of the molded plate was polished by about 20 μm. Also, the amount of moisture absorption and the coefficient of dynamic friction were measured.

実施例2 前述の処理中、脱脂前の乾燥、脱脂及び水蒸気による
除臭工程を省略した平均粒径30μmの天然皮革粉を用い
た以外は、実施例1と同様に、混合物シート及び成形品
での評価を行った。
Example 2 A mixture sheet and a molded product were prepared in the same manner as in Example 1 except that natural leather powder having an average particle size of 30 μm was used during the above-described treatment, in which the steps of drying before degreasing, degreasing and deodorizing with steam were omitted. Was evaluated.

実施例3 ゴムとして合成ゴム・EPDM(出光ディーエスエム社Ke
ltan314)を単独で100重量部とした以外は、実施例1と
同様に、混合物シートと成形品との評価を行った。
Example 3 As a rubber, synthetic rubber / EPDM (Keiko Idemitsu K.K.
The mixture sheet and the molded product were evaluated in the same manner as in Example 1 except that 100 parts by weight of tan 314) alone was used.

実施例4 ゴムとして天然ゴムを単独で100重量部とした以外
は、実施例1と同様に、混合物シートと成形品との評価
を行った。
Example 4 The mixture sheet and the molded product were evaluated in the same manner as in Example 1 except that the natural rubber alone was used as 100 parts by weight.

実施例5 ゴムとして天然ゴム80重量部、合成ゴム・EPDM20重量
部を用い、前述の処理をした天然皮革粉(平均粒径30μ
m)を25重量部用いた以外は、実施例1と同様に行っ
た。
Example 5 Using 80 parts by weight of natural rubber and 20 parts by weight of synthetic rubber / EPDM as rubber, the natural leather powder (average particle size 30 μ
Example 1 was repeated except that 25 parts by weight of m) was used.

実施例6 ペレット状の合成ゴム(シリコーンゴム)100重量部
と前述の処理をした天然皮革粉(平均粒径30μm)50重
量部とを150℃〜160℃の二本ロールで均一に混合し、シ
ート状の混合物を得、更に、このシート状の混合物をプ
レス成形機により約180℃に加熱しながら、厚さ2mmのシ
ート状成形板(150mm×150mm)を作製し、実施例1と同
様に、耐湿テスト、吸湿量、動摩擦係数等の測定を行っ
た。
Example 6 100 parts by weight of pellet-shaped synthetic rubber (silicone rubber) and 50 parts by weight of the above-treated natural leather powder (average particle size 30 μm) were uniformly mixed with a two-roll roll at 150 ° C. to 160 ° C., A sheet-shaped mixture was obtained, and a sheet-shaped forming plate (150 mm × 150 mm) having a thickness of 2 mm was prepared while heating the sheet-shaped mixture to about 180 ° C. by a press molding machine, and in the same manner as in Example 1. The moisture resistance test, the amount of moisture absorption, and the coefficient of dynamic friction were measured.

実施例7 天然ゴム20重量部及び合成ゴムEPDM80重量部と、前述
の処理をした天然皮革粉(平均粒径60μm)350重量部
とを用いた以外は、実施例1と同様に行った。
Example 7 Example 1 was repeated except that 20 parts by weight of natural rubber, 80 parts by weight of synthetic rubber EPDM, and 350 parts by weight of the natural leather powder (average particle size 60 μm) treated as described above were used.

比較例1 水洗処理を行っていない天然皮革粉(平均粒径60μ
m)を用いた以外は、実施例1と全て同じに作製し、得
た混合物シート及び成形板での評価を行った。
Comparative Example 1 Natural leather powder that has not been washed with water (average particle size 60μ
All were prepared in the same manner as in Example 1 except that m) was used, and the obtained mixture sheet and molded plate were evaluated.

比較例2 水洗処理を行っていない天然皮革粉(平均粒径30μ
m)を用いた以外は、実施例3と同様に混合物シート及
び成形板での評価を行った。
Comparative Example 2 Natural leather powder that has not been washed with water (average particle size 30μ
Evaluations were performed on the mixture sheet and the molded plate in the same manner as in Example 3 except that m) was used.

比較例3 平均粒径の小さな天然皮革粉(平均粒径5μm)を用
いた以外は、実施例1と同様に混合物シート及び成形板
での評価を行った。
Comparative Example 3 A mixture sheet and a molded plate were evaluated in the same manner as in Example 1 except that natural leather powder having a small average particle size (average particle size 5 μm) was used.

比較例4 平均粒径の大きな天然皮革粉(平均粒径300μm)を
用いた以外は、実施例3と同様に、混合物シート及び成
形板での評価を行った。
Comparative Example 4 A mixture sheet and a molded plate were evaluated in the same manner as in Example 3 except that natural leather powder having a large average particle size (average particle size 300 μm) was used.

比較例5 天然ゴム80重量部、合成ゴム・EPDM20重量部に、実施
例1と同様な天然皮革粉(平均粒径60μm)を450重量
部添加したところ、せん断発熱の増大と併せ、二本ロー
ルでのシート化が困難となった。
Comparative Example 5 To 80 parts by weight of natural rubber and 20 parts by weight of synthetic rubber / EPDM, 450 parts by weight of the same natural leather powder (average particle size 60 μm) as in Example 1 was added. It became difficult to make a sheet.

比較例6 少ない量の天然皮革粉(平均粒径30μm、5重量部)
を用いた以外は、実施例3と同様に、混合物シート及び
成形板での評価を行った。
Comparative Example 6 A small amount of natural leather powder (average particle size 30 μm, 5 parts by weight)
In the same manner as in Example 3 except that was used, the mixture sheet and the molded plate were evaluated.

比較例7 少ない量の天然皮革粉(平均粒径60μm、5重量部)
を用いた以外は、実施例4と同様に、混合物シート及び
成形板での評価を行った。
Comparative Example 7 A small amount of natural leather powder (average particle size 60 μm, 5 parts by weight)
In the same manner as in Example 4 except that was used, the mixture sheet and the molded plate were evaluated.

比較例8 天然皮革粉の代わりに、ゼラチン粉末(平均粒径30μ
m)を50重量部を用いて混合シートを作製し、その後所
定形状の成形板を作製した以外は、実施例3と同様に評
価を行った。
Comparative Example 8 Instead of natural leather powder, gelatin powder (average particle size 30μ
Evaluation was performed in the same manner as in Example 3 except that a mixed sheet was produced using 50 parts by weight of m) and then a molded plate having a predetermined shape was produced.

比較例9 天然ゴム(#3)80重量部及び合成ゴム・EPDM(Kelt
an314)20重量部のみを用い、皮革粉を用いずに混合シ
ート状にしたもので、成形板を作製し、実施例1と同様
に評価を行った。
Comparative Example 9 80 parts by weight of natural rubber (# 3) and synthetic rubber / EPDM (Kelt
an314) 20 parts by weight was used, and a mixed sheet was prepared without using leather powder. A molded plate was prepared and evaluated in the same manner as in Example 1.

比較例10 合成ゴム・EPDM(Keltan314)100重量部の成形板にて
実施例1と同様に各種評価を行った。
Comparative Example 10 Various evaluations were performed in the same manner as in Example 1 using a molded plate containing 100 parts by weight of synthetic rubber / EPDM (Keltan314).

以上の実施例及び比較例における組成及び試験結果
を、表−1に示した。
The compositions and test results in the above Examples and Comparative Examples are shown in Table-1.

表−1から判るように、実施例1〜7では、カッター
切断切口における粉落ち(皮革粉が成形品から離脱する
こと)がなく、30℃、95%RHの雰囲気中に24時間放置し
た耐湿テストにおいても、白粉の発生等の異常は生じな
い。また、23℃、80%RHの雰囲気中に3時間放置した後
の吸湿量は、未研磨品で3.1g/cm2以上、研磨品で3.5g/c
m2以上の値を示し、十分な吸湿性、換言すると放湿性を
有しているといえる。更に、動摩擦試験でも、動摩擦係
数が未研磨品で0.38kg以上、研磨品で0.45kg以上の値を
示し、十分なすべり防止効果があるといえる。また、実
施例2のように皮革粉の樹脂をしなくとも、特性上問題
は生じない。しかし、脱脂を行った方が、臭気の点等で
有利となる。
As can be seen from Table-1, in Examples 1 to 7, there was no powder drop at the cutter cutting edge (leather powder did not come off from the molded product), and the humidity resistance was left for 24 hours in an atmosphere of 30 ° C and 95% RH. Even in the test, abnormalities such as generation of white powder do not occur. The moisture absorption after standing for 3 hours in an atmosphere of 23 ° C and 80% RH is 3.1 g / cm 2 or more for unpolished products and 3.5 g / c for polished products.
It exhibits a value of m 2 or more, and can be said to have sufficient hygroscopicity, in other words, moisture release. Further, in the dynamic friction test, the coefficient of dynamic friction was 0.38 kg or more for the unpolished product and 0.45 kg or more for the polished product, which can be said to have a sufficient slip prevention effect. Further, even if the resin of the leather powder is not used as in Example 2, there is no problem in characteristics. However, degreasing is advantageous in terms of odor and the like.

一方、比較例1及び2は、皮革粉の水洗処理がないた
め、耐湿テスト時に白粉を生じ、比較例3は、皮革粉の
平均粒径が10μm未満である5μmと小さいため、吸湿
量が未研磨、研磨共に低くなっている。また、比較例4
は、皮革粉の平均粒径が300μmと大きいため、粉落ち
を生じた。更に、比較例5は、皮革粉の混合量が450重
量部と多いため、シート作製ができず、比較例6,7は、
皮革粉の混合量が共に5重量部と少ないため、吸湿量が
少なく、動摩擦係数も小さい。また、比較例8は、皮革
粉の代わりにゼラチン粉末を用い、比較例9,10は、共に
皮革粉が全く混合されていないため、耐湿テストにより
表面にベトツキを生じた。比較例9,10では、吸湿量、動
摩擦係数も小さい。
On the other hand, in Comparative Examples 1 and 2, white powder was produced during the moisture resistance test because the leather powder was not washed with water, and in Comparative Example 3, the average particle size of the leather powder was as small as 5 μm, which is less than 10 μm. Both polishing and polishing are low. In addition, Comparative Example 4
Had a large average particle size of leather powder of 300 μm, and thus powder was removed. Further, in Comparative Example 5, since the amount of the leather powder mixed was as large as 450 parts by weight, it was not possible to prepare a sheet, and Comparative Examples 6 and 7
Since the amount of leather powder mixed is as small as 5 parts by weight, the amount of moisture absorption is small and the coefficient of dynamic friction is also small. Further, in Comparative Example 8, gelatin powder was used instead of leather powder, and in Comparative Examples 9 and 10, no leather powder was mixed at all, so that the surface was sticky due to the moisture resistance test. In Comparative Examples 9 and 10, the moisture absorption amount and the dynamic friction coefficient are also small.

以上の結果から、本発明の実施例によれば、従来の皮
革粉含有ゴム組成物でみられた白粉の発生を防止できる
効果がある。また、皮革粉含有のゴム成形品でベトツキ
感がなく、ラケット、ハンドル、筆記具、弦楽器ネック
部等におけるグリップ類では、握ったときすべり難くな
り、スポーツ用品、車両用部品、文房具、楽器等として
好適な性能を付与できる。更に、皮革粉含有のゴム成形
品で、衣料用手袋、帽子、ゴム靴、楽器吊下用ベルト等
を作製した場合、人の膚と接して汗を発生したとき、膚
に密着することが少なくなり、容易に脱ぐことができる
ようになる。また、本発明の組成物を用い車両内装品、
建材、家電製品、家具等の表面材を作製した場合、皮革
様外観による高級品を与えるのみならず、タッチ感が良
好になる。
From the above results, according to the examples of the present invention, it is possible to prevent the generation of white powder which is observed in the conventional leather powder-containing rubber composition. In addition, it is a rubber molded product containing leather powder that does not have a sticky feeling, and grips such as rackets, handles, writing instruments, and necks of stringed instruments make it difficult to slip when gripped, making it suitable for sports equipment, vehicle parts, stationery, musical instruments, etc. It is possible to add excellent performance. Furthermore, when rubber gloves containing leather powder are used to make clothing gloves, hats, rubber shoes, belts for hanging musical instruments, etc., when sweat occurs in contact with human skin, it does not tend to adhere to the skin. You can easily take it off. In addition, vehicle interior parts using the composition of the present invention,
When a surface material such as a building material, a home electric appliance, or furniture is manufactured, not only a high-quality product with a leather-like appearance is provided, but also a touch feeling is improved.

〔発明の効果〕〔The invention's effect〕

以上のような本発明によれば、白粉の発生がなく、表
面性状に優れた長期性能及び品質を有する皮革粉含有ゴ
ム組成物及び成形品を提供できるという効果がある。
According to the present invention as described above, there is an effect that it is possible to provide a leather powder-containing rubber composition and a molded product which do not generate white powder and have long-term performance and quality excellent in surface properties.

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平1−306446(JP,A)) 特開 昭63−178150(JP,A) 特開 平1−197600(JP,A) 特開 平2−219836(JP,A) 特開 昭64−56800(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (56) Reference JP-A-1-306446 (JP, A) JP-A-63-178150 (JP, A) JP-A-1-197600 (JP, A) JP-A-2 -219836 (JP, A) JP-A-64-56800 (JP, A)

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】皮質分が75wt%以上、水で抽出可能なNa+
イオンとCa2+イオンとの合計量が0.5wt%以下、及び平
均粒径D50が10μm〜250μmである皮革粉10〜400重量
部と、ゴム100重量部との分散混合物からなることを特
徴とする皮革粉含有ゴム組成物。
1. A water-extractable Na + having a cortical content of 75 wt% or more.
Characterized by comprising a dispersed mixture of 10 to 400 parts by weight of leather powder having a total amount of ions and Ca 2+ ions of 0.5 wt% or less and an average particle diameter D 50 of 10 to 250 μm, and 100 parts by weight of rubber. A rubber composition containing leather powder.
【請求項2】請求項1に記載の皮革粉含有ゴム組成物を
主として用いて成形されたことを特徴とする皮革粉含有
ゴム成形品。
2. A leather powder-containing rubber molded article, which is molded mainly using the leather powder-containing rubber composition according to claim 1.
JP2276733A 1990-10-15 1990-10-15 Rubber composition containing leather powder and molded article Expired - Lifetime JPH082997B2 (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
JP2276733A JPH082997B2 (en) 1990-10-15 1990-10-15 Rubber composition containing leather powder and molded article
US07/776,076 US5272190A (en) 1990-10-15 1991-10-11 Rubber composition containing powdered leather and molding products
TW080108055A TW218886B (en) 1990-10-15 1991-10-12
AU85821/91A AU639149B2 (en) 1990-10-15 1991-10-14 Rubber composition containing powdered leather and molding products
KR1019910018027A KR0128515B1 (en) 1990-10-15 1991-10-14 Leather powder-containing rubber compositions and molded articles
DE69119349T DE69119349T2 (en) 1990-10-15 1991-10-15 Rubber composition containing leather in powder form
EP91117582A EP0481430B1 (en) 1990-10-15 1991-10-15 Rubber composition containing powdered leather and molding products

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2276733A JPH082997B2 (en) 1990-10-15 1990-10-15 Rubber composition containing leather powder and molded article

Publications (2)

Publication Number Publication Date
JPH04149254A JPH04149254A (en) 1992-05-22
JPH082997B2 true JPH082997B2 (en) 1996-01-17

Family

ID=17573588

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Application Number Title Priority Date Filing Date
JP2276733A Expired - Lifetime JPH082997B2 (en) 1990-10-15 1990-10-15 Rubber composition containing leather powder and molded article

Country Status (7)

Country Link
US (1) US5272190A (en)
EP (1) EP0481430B1 (en)
JP (1) JPH082997B2 (en)
KR (1) KR0128515B1 (en)
AU (1) AU639149B2 (en)
DE (1) DE69119349T2 (en)
TW (1) TW218886B (en)

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Also Published As

Publication number Publication date
DE69119349D1 (en) 1996-06-13
AU639149B2 (en) 1993-07-15
EP0481430A3 (en) 1992-08-12
DE69119349T2 (en) 1996-11-07
EP0481430A2 (en) 1992-04-22
US5272190A (en) 1993-12-21
TW218886B (en) 1994-01-11
JPH04149254A (en) 1992-05-22
KR0128515B1 (en) 1998-04-04
AU8582191A (en) 1992-04-16
KR920008124A (en) 1992-05-27
EP0481430B1 (en) 1996-05-08

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